1. Field of the Invention
The present invention relates to co-injection molding machines, methods for forming co-injected hollow plastic structures and the resulting articles formed thereby.
2. Background Art
A variety of approaches have been taken to manufacture structural elongate plastic members in order to provide the necessary structure, while controlling part cost. An area in which plastic elongate structures are gaining in popularity is in the fabrication of railing systems for decks and porches. The trend toward plastic railing systems is driven primarily by the demand for a maintenance free deck or porch. While it is relatively simple to manufacture the horizontal hand rail and bottom rail in a railing system out of an aluminum structural extrusion capped with a separately extruded vinyl member, non-axially uniform posts and spindles cannot be so easily fabricated. Typically, posts for a vinyl railing system are simple vinyl extrusions telescopically fit over a wood post. Alternatively, vinyl can be overmolded about a wood post by injection molding. In order to avoid rot, chemically pressured treated wood is preferably used.
The spindles which vertically span between the hand rail and the lower rail in a rail system are commonly fashioned to resemble traditional turned wood spindles. This configuration can be achieved in plastic by blow molding a vinyl tubular extrusion which is heated and inserted into a closed molded desired shape and inflated to conform to the mold interior periphery. While complex shapes can be achieved using this blow molding technique, the resulting tubular vinyl product, if provided with a very thick wall, becomes expensive and if provided with a thin wall, lacks structural rigidity. Alternative approaches have been utilized to provide a structural spindle such as insert injection molding a plastic exterior about a wood or steel rod insert. However, these designs are expensive and heavy.
The applicant seeks to design a system and method capable of manufacturing low cost structural members having an exterior surface provided by a thin layer of appearance quality plastic having a good appearance and environmental properties with an interior formed of a rot resistance light-weight low cost material.
The present invention includes a system and method for plastic injection molding elongate structural members and the resulting articles molded thereby, particularly well suited for, but not limited to structural railing members such as railing posts and railing spindles. One embodiment of the invention is provided by a plastic injection molding system which includes a mold clamp adapted to receive a mold for forming a plastic part. The mold has at least two sections movable relative to one another by a mold clamp actuator. A co-extruded unit feeds fluid plastic into the mold cavity. The co-extruder at least two plastic extruders, each having a different plastic material source and at least one outlet communicating with mold cavity. The fluid assist unit is further provided for providing a controllable metered injection of pressurized gas or liquid into the mold cavities sequentially following the injection of metered quantities of each plastic fluid. The controller regulates the operation of the mold clamp, the two plastic extruders and the gas or liquid assist unit to form a hollow plastic part having an exterior shell of a first material and an inner structural shell of a second plastic material and an internal hollow cavity all formed in a single molding station.
Preferably, each of the two plastic extruders in the co-extruder unit are each provided with a heater for heating thermoplastic material to a fluid state and a pump for transferring pressurized plastic fluid from the extruders through the outlet nozzle and to the mold cavity.
The method of forming a molded elongate article includes the step of providing a mold for forming an elongate structural member and installing the mold in a dual injection molding machine which is provided with a gas or fluid assist system. A metered amount of a first fluid plastic material is injected into the mold partially filling the cavity and contacting the mold cavity walls. Next, a second fluid plastic material, which is different than the first plastic material, is injected into the mold cavity displacing the first plastic material along the mold in contact with the mold walls forming a thin layer separating the second plastic material from the mold. Finally, pressurized gas is injected into the center of the mold occupied by the second fluid plastic material forming an axially elongate cavity and displacing both the first and second plastic materials from the entire length of the mold with the first material in contact with the mold wall to form a thin layer of first material separating the second layer of material from the mold walls. The pressurized gas is then vented and the molded part is removed from the mold cavity.
Preferably, the method is carried out utilizing a first and second thermoplastic material which are heated in the co-extruder machine to a fluid state. Ideally, the first fluid plastic material is in appearance quality UV stable thermoplastic such as vinyl. The second plastic material may be of lower cost thermoplastic with good structural properties such as fiber filled recycled thermoplastic.
The invention is further directed toward elongate structural members particularly, elongate railing members such as railing posts and railing spindles. The elongate members are provided with a thin tubular plastic skin layer of a first appearance quality material forming an exterior surface and a plastic inner layer of a second structural member different from the outer skin and formed conformably to the plastic outer layer and defining a hollow elongate internal cavity in a single molding operation. Preferably, the first and second plastic materials are thermoplastic such as a vinyl outer layer and a fiber reinforced recycled thermoplastic inner layer.
a-3d illustrate a sequential series of steps in which a spindle of the present invention is formed in a single molding operation;
a through 3d illustrate a series of plastic injection steps utilized to form spindle 20 of
Following the injection of the first plastic material, a second plastic material 40 is injected through the injection nozzle 34. The introduction of the second fluid plastic material 40 causes the first fluid plastic material 38 to translate axially along mold cavity 32 contacting the walls of the mold and forming a thin plastic layer adjacent the mold wall as illustrated. The second fluid plastic material and the first fluid plastic material collectively, take up less than all of the interior cavity volume as illustrated in
The co-extruder 56 is provided with at least two plastic extruders, 58 and 60, each providing a different plastic material to at least one outlet nozzle 62 which cooperates with the mold internal cavity. Co-extruders of this general type are known in the art and are illustrated in U.S. Pat. Nos. 4,609,516; 4,470,936; 4,715,802; and 4,722,679, all four of which are incorporated by reference herein for the purpose of illustrating co-extruder (co-injection) molding machines.
When thermoplastic material is to be used, each of the plastic extruders 58 and 60 will be provided with a heater for heating plastic material to a fluid state and a fluid pump such as a rotary auger or a piston ram for pressurizing the fluid plastic material and injecting the material through the injector nozzle 64 into the molded internal cavity. The co-extruder 56 introduces a controlled amount of each of the fluid plastic materials sequentially into the mold cavity. A gas assist system 64 is provided having a gas injection pin 36 illustrated in
The fluid assist unit includes a regulator valve 66 to control the flow of pressurized gas or liquid from a supply line 68 into the mold cavity as described previously following the step of injecting meter quantities of each of the fluid plastic materials. A controller 70 is provided for regulating the sequential operation of the mold clamp, the two plastic extruders, and the gas assist unit to form a hollow part having an exterior shell made of a first plastic material and an inner structural shell of the second plastic material. The second plastic material is conformably molded in situ with the first plastic material about a central hollow cavity in a single molding operation. The controller 70 may be a single controller or may be two or more controllers with logic distributed throughout the system. Controller 70 may be connected to the other components of the system via hard wiring, a wireless network or through an ethernet or fiber optic network. Preferably, the controller will monitor the system's pressures and temperatures and the movement of the mold and the injector pins enabling the automatic manufacture of molded articles.
An alternative dual injection plastic molding system 72 is illustrated in
Co-extruder 74 is specifically adapted to sequentially inject two different plastic materials into a mold in uninterrupted succession eliminating any hesitation marks in the final part resulting from the transition between different extruder heads. Co-extruder 74 is provided with a heated elongate cylindrical barrel 76 having an internal bore sized to receive an elongate feed screw 78 which is rotatably driven by a motor 80. Feed screw 78 has two separate screw auger regions; a forward region 82 and a rearward region 84 which are separated by a central land 86. A forward spiral chamber 88 is formed between the forward screw 82 and the cylindrical inner bore of barrel 76. Forward spiral chamber 88 is fed a first plastic material 90 through a radially extending port 92. A second spiral chamber is formed between the rearward screw portion 84 and the inner bore of barrel 76. A second material 96 is fed into rearward spiral chamber 94 via a feed port 98. Screw 78 is provided with a central axial passage 100 having an inlet port 102, rearward of land 86 opening into the forward most region of the spiral chamber 94 and an outlet 104 at the distal end of screw of 78.
In operation, as screw 78 is rotated by motor 80, the first plastic material 90 enters the forward spiral chamber 88 via port 92 where the plastic is heated to a fluid state and forwardly driven as a result of the screw rotation. Similarly, the second plastic material 96 enters the rearward spiral chamber 94 via port 98 where it is heated to a fluid state and driven forward by the rotation of the rearward screw segment 84. The plastic cannot flow beyond land 86 causing the plastic to enter inlet port 102 and flow axially to the outlet port 104. While screw 78 is being rotated by motor 80 in
When a substantial portion of the second plastic material is injected into mold 106, through nozzle 108, assist fluid valve 110 is opened allowing the fluid such as a pressurized gas or alternatively, a pressurized liquid is injected into the center of a second fluid plastic material 96 to form an internal cavity 112 as illustrated in
It should be further appreciated that the co-axial co-injection unit 74 described in reference to
While
In order to manufacturer elongate extruded objects according to the present invention, one must establish process control settings for the particular materials to be used, the part shape and the desired finished part geometry. For example, the thickness of the vinyl layer will depend upon the temperature of the vinyl melt at the time of injection, the mold wall temperature, and the rate of injection. Similarly, the wall thickness of the structural material will depend upon the material melting temperature, the material temperature at the time of injection, the rate of injection as well as the fluid assist pressure. The amount of structure material and the ends of the elongate member is dictated by the wall thickness as described above, the mold cavity volume and the charge volume of the structural material. The larger the charge volume, the greater the concentration of structural material and the distal end of the part. The amount of structural material in the proximate end of the part is dictated, at least in part, by the fluid assist injection pin length. The process control parameters for a specific part to be formed can be readily determined by routine experimentation by one of ordinary skill in the injection molding field.
While embodiments of the invention have been illustrated and described, it is not intended that these embodiments illustrate and describe all possible forms of the invention. Rather, the words used in the specification are words of description rather than limitation, and it is understood that various changes may be made without departing from the spirit and scope of the invention.